Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems

ABSTRACT

Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems are a closed-type precision media system. The aqueous slurry type system pumps aqueous slurry Electrolyte from an aqueous slurry pump. The differential pressurized variable control regulation closed-type system utilizes negative pressurized air drawing media from a powerful control valve or control valve venturi and vacuum pump. The Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems are light and easy to operate opening the door to whole new market of customers to safely perform paint stripping, substrate treatment, parts treatment and cleaning specifications. Efficiency of operation is acquired by way of diffusion, equal particle distribution, and the effective Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems can compete against harmful paint thinners, petroleum distillates, and chemical cleaners.

DOMESTIC PRIORITY DATA

This is an application a continuation in part of preliminary amendment to specification application Ser. No. 13/452,885 Filing Date Apr. 22, 2012.

BACKGROUND OF THE INVENTION

Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems are a replacement for hazardous materials solvents, paint thinners, and chemicals. Solvents, petroleum distillates, and paint thinners are categorized as carcinogen and hazardous materials. Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems are designed to safely clean parts and remove paint by physico-chemical means as opposed to harmful chemicals.

Many of the abrasive hoppers on the market today are bulky, heavy, and are hard to operate. Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems are light and easy to use, opening the door to whole new market of customers to safely perform paint stripping, substrate treatment, parts treatment and cleaning specifications.

BRIEF SUMMARY OF THE INVENTION

Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems are simple in design, light, and easy to operate for many specific cleaning, and coating removal applications. This system should find success as environmentally and health conscious consumers become aware of the risks of using hazardous materials. In addition to the consumer market this system may be utilized in the automotive and aerospace industry highly technical paint stripping, substrate treatment, parts treatment and cleaning specifications providing an environmental incentive for business that is change for the better.

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWING FOLLOWS FIGURES 1 TO 13

FIG. 1 Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems airtight plastic injection molded preformed gravity feed free flow hopper comprising lid with release valve, air filter, silica gel slots, and filtered air gravity feed outlet sizes may vary;

FIG. 2 Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems airtight plastic injection molded preformed gravity feed bottom free flow hopper comprising lid with release valve, air filter, silica gel slots, and filtered air top feed outlet sizes may vary;

FIG. 3 Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems airtight plastic injection molded preformed gravity feed float free flow hopper comprising lid with release valve, air filter, silica gel slots, and filtered air top feed outlet sizes may vary;

FIG. 4 differential pressurized variable control regulation Surface Treat and Survey Substrate Substances Renewable Food Starch, Sodium and Electrolyte Precision Media System;

FIG. 5 differential pressurized variable control regulation Surface Treat and Survey Substrate Substances Renewable Food Starch, Sodium and Electrolyte Precision Media System;

FIG. 6 zero nozzle aqueous slurry Substrate Substances Renewable Food Starch, Sodium and Electrolyte Precision Media Systems vertical alignment, or standard alignment shape nozzle aperture measured in diameter, divergence measured in degrees angulation or linear, aperture measured in diameter, six to ten sides or continuous measured in diameter not shown here;

FIG. 7 Parallel phase differential pressurized variable control regulation Surface Treat and Survey Substrate Substances Renewable Food Starch, Sodium and Electrolyte Precision Media System;

FIG. 8 Standard nozzle measured in diameter sizes may vary with fine water suppressor;

FIG. 9 Encapsulated pressurized nozzle with fine water suppressor;

FIG. 10 Alternating encapsulated pressurized nozzle with fine water suppressor;

FIG. 11 Zero encapsulated nozzle differential pressurized variable control regulation Substrate Substances Renewable Food Starch, Sodium and Electrolyte Precision Media System;

FIG. 12 Zero standard nozzle differential pressurized variable control regulation Substrate Substances Renewable Food Starch, Sodium and Electrolyte Precision Media System; and

FIG. 13 Differential pressurized variable control regulation Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems with 4× expansion of control valve or control valve venturi.

DETAILED DESCRIPTION OF THE DRAWINGS FIGURES 1 TO 13

FIG. 1 lid with release valve, air filter, silica gel slots, and filtered air gravity feed outlet, FIG. 2 Lid with release valve, air filter, silica gel slots, filtered air top feed outlet, and gravity feed bottom, FIG. 3 Lid with release valve, air filter, silica gel slots, filtered air top feed outlet, and gravity feed float, FIG. 4 1—Compressed air hose line-in measured in diameter, 2—Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 3—Outer pressurized chamber, 4—Variable control regulator, 5—Inner pressurized chamber, 6—Variable control regulator, 7—Compressed air and Renewable Food Starch, Sodium and Electrolyte hose line-out measured in diameter, 8—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, and 9—Encapsulated nozzle, FIG. 5 1—Compressed air hose line-in measured in diameter, 2—Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 3—Stage one pressurized chamber, 4—Variable control regulator, 5—Compressed air and Renewable Food Starch, Sodium and Electrolyte hose line-out measured in diameter, 6—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, and 7—Encapsulated nozzle, FIG. 6 1—Specification aqueous slurry pliable hose line-in measured in diameter from aqueous slurry electronic pump finite or variable control delimited not shown here; 2—specification aqueous slurry pliable hose line-in measured in diameter; 3—specification of pressurized air hose line-in measured in diameter from electronic air compressor pump finite or variable control delimited not shown here; 4—bi-interval valve measure in diameter not shown here; 5—specification of pressurized air hose line-in measured in diameter to vertical alignment encapsulated nozzle or standard alignment encapsulated nozzle not shown here; 6—vertical alignment encapsulated nozzle; and 7—vertical alignment shape nozzle aperture measured in diameter, divergence measured in degrees angulation or linear, aperture measured in diameter, six to ten sides or continuous measured in diameter sizes may vary not shown here, FIG. 7 1—Compressed air hose line-in measured in diameter, 2—Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 3—Compressed air hose line-in measured in diameter, 4—Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 5—Outer pressurized chamber, 6—Variable control regulator, 7—Inner pressurized chamber, 8—Variable control regulator, 9—Outer pressurized chamber, 10—Variable control regulator, 11—Inner pressurized chamber, 12—Variable control regulator, 13—Compressed air and Renewable Food Starch, Sodium and Electrolyte hose line-out 1 measured in diameter, 14—Compressed air and Renewable Food Starch, Sodium and Electrolyte hose line-out 2 measured in diameter, 15—Parallel phase regulator switch; elbow connectors; hose line-in measured in diameter, 16—Compressed air and Renewable Food Starch, Sodium and Electrolyte hose line-out 1-2 measured in diameter, 17—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, and 18—Encapsulated nozzle, FIG. 8 1—Compressed air and Renewable Food Starch, Sodium and Electrolyte hose line-out measured in diameter, 2—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, and 3—Standard nozzle measured in diameter sizes may vary, FIG. 9 1—Pressurized air and Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 2—Encapsulated nozzle O-ring regulator pneumatic connector finite control, 3—Encapsulated nozzle pressurized chamber, 4—Encapsulated nozzle regulator 2 aperture measured in diameter, 5—Nozzle measured in diameter sizes may vary, and 6—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, FIG. 10 1—Pressurized air and Renewable Food Starch, Sodium and Electrolyte hose line-in 1 measured in diameter, 2—Pressurized air and Renewable Food Starch, Sodium and Electrolyte hose line-in 2 measured in diameter, 3—Encapsulated nozzle O-ring regulator pneumatic connector finite control 1, 4—Encapsulated nozzle O-ring regulator pneumatic connector finite control 2, 5—Alternating encapsulated nozzle regulator 2 aperture 1 measured in diameter, 6—Alternating encapsulated nozzle regulator 2 aperture 2 measured in diameter, 7—Nozzle measured in diameter sizes may vary, 8—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, 9—Pressurized chamber encapsulated nozzle 1, and 10-Pressurized chamber encapsulated nozzle 2, FIG. 11 Lid with release valve, air filter, silica gel slots, and filtered air gravity feed outlet, 1—Compressed air hose line-in measured in diameter; Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 2—Encapsulated nozzle O-ring regulator pneumatic connector finite control, 3—Encapsulated nozzle pressurized chamber, 4—Encapsulated nozzle regulator 2 aperture measured in diameter, 5—Encapsulated nozzle measured in diameter sizes may vary, 6—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, 7—Control valve Renewable Food Starch, Sodium and Electrolyte hose line-out measured in diameter, 8—Variable compressed air regulator hose line-in measured in diameter control valve, and 9‘3Control valve, FIG. 12 Lid with release valve, air filter, silica gel slots, and filtered air gravity feed outlet, 1—Compressed air hose line-in measured in diameter; Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 2—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, 3-Standard nozzle measured in diameter sizes may vary, 4—Control valve Renewable Food Starch, Sodium and Electrolyte hose line-out measured in diameter, 5—Variable compressed air regulator hose line-in measured in diameter control valve, and 6—Standard nozzle drilled bore-hole measured in diameter, and FIG. 13 Lid with release valve, air filter, silica gel slots, and filtered air gravity feed outlet, 1—Compressed air hose line-in measured in diameter, 2—Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 3—Outer pressurized chamber, 4—Variable control regulator, 5—Inner pressurized chamber, 6—Variable control regulator, 7—Compressed air line-out measure in diameter; Renewable Food Starch, Sodium and Electrolyte hose line-out measured in diameter, 8—Water hose line-in measured in diameter fine water suppressor water ring or water ring delimited, 9—Encapsulated nozzle, 10—Control valve Renewable Food Starch, Sodium and Electrolyte hose line-in measured in diameter, 11—Control valve, 12—Control valve Renewable Food Starch, Sodium and Electrolyte hose line-out measured in diameter, and 13—Variable compressed air regulator hose line-in measured in diameter control valve.

DETAILED DESCRIPTION OF THE INVENTION

Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems first are a physico-chemical means to safely clean, degrease, and coating removal from parts and substrates such as metals, alloys, copper, glass, unreinforced masonry URMs, stone, concrete, and asphalt. These systems are light, easy to use and extremely efficient air pressurized system that utilizes Renewable Food Starch, Sodium and Electrolyte.

All parts Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems are built to specification towards the application specificity requirement and conform with the specified requirements to a unique American Society for Testing and Materials ASTM International Standards Worldwide identifiers and sizes may vary.

Description of all parts making and using the same built to specification towards the application specificity requirement sizes may vary for Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems 1. Renewable Food Starch, Sodium and Electrolyte airtight plastic injection molded preformed gravity feed free flow hopper comprising lid with release valve, air filter, silica gel slots, any combination of cone or parabolic shaped bottom variations for the Renewable Food Starch, Sodium and Electrolyte consistency and size measured in mesh, filtered air gravity feed outlet, or filtered air top feed outlet with or without gravity feed float, or vacuum packed sealed plastic bag; 2. Control valve or control valve venturi, specification of negative pressurized air, specification of compressed air control, and specification of pneumatic hose line-in and line-out measured in diameter with or without electric blower variable control; 3. Specification pneumatic hose line-in measured in diameter, and specification of compressed air; 4. Outer pressurized chamber, specification of compressed air, and variable control regulator compressed air control; 5. Inner pressurized chamber, specification of compressed air, and variable control regulator compressed air control; 6. Specification pneumatic hose line-out measured in diameter; 7. Parallel phase regulator switch, specification of compressed air control, specification pneumatic hose line-in left and right measured in diameter, and elbow connectors left and right; 8. Encapsulated nozzle, specification of pressurized air, encapsulated nozzle O-ring regulator pneumatic connector finite control, encapsulated nozzle regulator 2 specification of compressed air regulated control, nozzle attachments measured in diameter, and aperture measured in diameter; or alternating encapsulated nozzle, alternating encapsulated nozzle two specifications of pressurized air, alternating encapsulated nozzle two O-ring regulators pneumatic connectors finite control, alternating encapsulated nozzle two regulators 2 specification of compressed air regulated control, nozzle attachments measured in diameter, and aperture measured in diameter; or encapsulated fan nozzle for applications requiring a wide stream of Renewable Food Starch, Sodium and Electrolyte for paint stripping, substrate treatment, parts treatment and cleaning specifications of pressurized air, encapsulated nozzle O-ring regulator pneumatic connector finite control, encapsulated nozzle regulator 2 specification of compressed air regulated control, fan nozzle attachments measured in diameter, and aperture measured in diameter; or shop vacuum pump wet and dry plastic injection molded preformed cone shaped and contoured vacuum attachments affixed at the end of the nozzle by way of a shop vacuum pump wet and dry hose line-in measured in diameter; 9. Wand with nozzle, siphon, or pump, and nozzle attachments measured in diameter; 10. Water suppressor supply of water hose line-in measured in diameter and fine water suppressor attachments water ring or water ring delimited; 11. Nozzle measured in diameter specification of pressurized stream; 12. Plastic injection molded preformed parts cleaning cabinet system; diminishing gravity feed bottom and attachments of the parts cleaning cabinet system not shown here; 13. Naturally occurring Sodium nitrate NaNO₃ and Sodium Chloride NaCl are derived from natural and renewable resources. All sodium salts are highly soluble renewable source of sodium extracts available in thousands of tons per annum are found in shell fish. Since the only guide to the desirable upper limit of sodium is based upon sodium absorption ratio in common use measure of the proportion of sodium relative to beneficial elements calcium and magnesium the complex ratio can be largely found in shell fish principally clams and oyster shells that are crushed and pulverized to powder and batch processed pasteurization then screened in fine mesh range cloths removing non liquid soluble material while sodium salt is dissolved in water ionizing to sodium ions Na⁺ and the other part as an anion negative charge so that the sodium then acts independently of the anion, although influenced by salinity and pH. The water is removed by melting and boiling point temperatures, latent evaporation condensing, and fractional distillation to the purity of salt crystalline fine white crystalline powder screened and classified for metallurgy surface treatment, increase yields are also made by the high gelling ability in the presence of calcium citrates chelation of the calcium ions by the citrate ions results in the formation of calcium citrate with sodium ion complexes that are synthesis dilute extraction. 14. Byproducts of the fruit processing industry are the primary media food ingredient citrus peels, pulps, seeds, and banana peels that are picked-up from large fruit processing plants in carbon dioxide refrigerated trucks. The mass fibrous agricultural waste are specially handled and dumped into vacuum pressurized vats beginning the batch process with dehydration low heating evaporation, and/or supercooled disintegrated to form organogenic crystallographic network and/or crushed, pulverized and classifier screened into grade white crystalline powder base, solution batch classifiers solution batch separate liquid soluble from non liquid soluble material from universal pulp pressing, screening and filtration for clarification non liquid soluble from liquid soluble and/or from dilute extraction soluble. The liquid soluble solutions are suspended in three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch. The three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch solutions may be chemically dehydrated, supercooled disintegrated to form organogenic crystallographic network and classifier screened into grade white crystalline powder base, or low heating evaporated into fine white crystalline powder. The non liquid soluble pulps may be supercooled disintegrated to form organogenic crystallographic network or crushed and classifier screened into three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch and may repeat filtration for clarification non liquid soluble from liquid soluble and/or from dilute extraction soluble. The three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch also may be carbon dioxide super cooled to 0° C. or 32° F. temperatures super cooling refrigeration decelerate temperature to −109° F. degrees Fahrenheit or −78.5° C. degrees Celsius forming organogenic crystallographic network. The three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch may be classifier screened into organogenic crystallographic network grade white crystalline powder or supercooled disintegrated to form organogenic crystallographic network or crushed, pulverized and classifier screened into grade white crystalline powder base, and/or from dilute extraction soluble. Base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate are initiated by fermentation of peel, pulps and seeds proteins pecin, and pecin citric acid category or sodium citrate category white crystalline powder, cultivated in Vats with the mould Aspergillus niger, incubated with warm heat on ⅛ diurnal cycle incremental mould Aspergillus niger cultivate and lasting for a few days.

-   Step-1 Sodium citrate is formed from reactions of carbonate ions     with citric acid and are chelated by the citrate ion of sodium     citrate, the process of organic compounds form multiple bonds with a     single metal ion, resulting in the formation of complex molecules     that are highly soluble, inactive non reacting with other elements     or ions to produce precipitates. -   Step-2 Sodium citrate increase yields are also made by the high     gelling ability in the presence of calcium citrates chelation of the     calcium ions by the citrate ions results in the formation of calcium     citrate with sodium citrate complexes that are dilute extraction     soluble. With crystallization techniques and including the sodium     citrate chelating technique results in E Number E330 citric acid     grade white crystalline powder made in anhydrous form having the     property to crystallize from hot water or monohydrate form having     the property to crystallize from cold water. Likely the monohydrate     form can be converted to the anhydrous form with high heating. The     Food Starch, Sodium and Electrolyte base white crystalline powder     and liquids comprise a remarkable consecutive incremental yield as     many as 8%, 16%, 24% and 48% of the weight of the fruit industry     byproduct.

Description of all parts making and using the same built to specification towards the application specificity requirement sizes may vary Renewable Food Starch, Sodium and Electrolyte aqueous slurry formula zero nozzle aqueous slurry system; 1—Specification aqueous slurry pliable hose line-in measured in diameter from aqueous slurry electronic pump finite or variable control delimited not shown here; with or without specification of pressurized air hose line-in measured in diameter from electronic air compressor pump finite or variable control delimited not shown here; and with or without specification of pressurized air hose line-in measured in diameter to vertical alignment encapsulated nozzle or standard alignment encapsulated nozzle not shown here; 2—with or without bi-interval valve measured in diameter not shown here; and 3—encapsulated nozzle vertical alignment shape nozzle or vertical alignment shape nozzle without encapsulated nozzle aperture measured in diameter, divergence measured in degrees angulation or linear, aperture measured in diameter, or encapsulated nozzle standard alignment shape nozzle or standard alignment shape nozzle without encapsulated nozzle aperture measured in diameter, divergence measured in degrees angulation or linear, aperture measured in diameter, six to ten sides or continuous measured in diameter not shown here.

The specification as set forth comprises electrical component systems rated alternating AC or direct current DC attached to a portable frame with handles and wheels not shown here; electric motor, air compressor, power supply, rated volts alternating current AC; electric motor, vacuum pump, power supply rated volts alternating current AC; electric motor oscillator, power supply rated volts alternating current AC, or pneumatic oscillator, and pressurized variable control air hose line-in measured in diameter; electric motor, vacuum pump wet or dry, power supply rated volts alternating current AC; and an aqueous slurry electronic motor pump finite or variable control delimited, power supply rated volts alternating current AC, or direct current DC battery power; electronic air compressor pump finite or variable control delimited, power supply rated volts alternating current AC, or direct current DC battery power not shown here.

The Renewable Food Starch, Sodium and Electrolyte airtight plastic injection molded preformed gravity feed free flow hopper comprising lid with release valve, air filter, silica gel slots, and filtered air gravity feed outlet or filtered air top feed outlet, or vacuum packed sealed plastic bag is utilized specially packaged closed recycled refilled preparation Renewable Food Starch, Sodium and Electrolyte.

The plastic gravity feed free flow hopper, or vacuum packed sealed plastic bag variations for the Renewable Food Starch, Sodium and Electrolyte consistency and size measured in mesh may or may not sit in an oscillator not shown here that oscillates to and fro allowing the Renewable Food Starch, Sodium and Electrolyte to evenly distribute over the gravity feed bottom to an opening located in the center.

The Renewable Food Starch, Sodium and Electrolyte airtight plastic injection molded preformed gravity feed free flow hopper comprising lid with release valve, air filter, silica gel slots, any combination of cone or parabolic shaped bottom, or vacuum packed sealed plastic bag variations for the Renewable Food Starch, Sodium and Electrolyte consistency and size measured in mesh, filtered air gravity feed outlet, or filtered air top feed outlet with or without gravity feed float connects directly to the control valve or control valve venturi FIGS. 11, 12, and 13 or to the control valve or control valve venturi inside of a plastic injection molded preformed parts cleaning cabinet system not shown here combined with zero nozzle system encapsulated nozzle pressurized air, or zero nozzle system standard nozzle pressurized air whereby it cleans, remove contamination, and coating removal from parts and desired substrates such as metals and alloys. Remaining debris are drawn into diminishing gravity feed bottom of the parts cleaning cabinet by way of a shop vacuum pump wet and dry hose line-in measured in diameter and attachments not shown here. A siphon, or pump and attachments are added to any nozzle for environmentally responsible liquid electrolyte rinsing and cleaning not shown here.

Renewable Food Starch, Sodium and Electrolyte are drawn into the Renewable Food Starch, Sodium and Electrolyte line-in measured in diameter by way of negative pressurized air and transported directly into the control valve or control valve venturi and projected freely into the pressure system whereby it reaches specification diffusion and achieves equal particle distribution.

After the Renewable Food Starch, Sodium and Electrolyte exits the encapsulated nozzle or standard nozzle there it can be suppressed by water to clean and remove contamination from the desired substrate. The Renewable Food Starch, Sodium and Electrolyte and contamination can be vacuumed up by way of a shop vacuum pump wet and dry hose line-in measured in diameter plastic injection molded preformed cone shaped and contoured vacuum attachment affixed at the nozzle not shown here.

This system comprises air pressurized chambers, variable control regulation, and a dual regulation standard. Differential pressurization are the process obtaining diffusion with equal particle distribution for one, two, or more pressurized streams combined FIGS. 4, 5, 7, 9, 10, 11, 12, and 13.

Differential pressurization can be mathematically determined in cubic feet per minute CFM and pounds per square PSI for the following four systems 1. Zero system specification air pressurization, control valve variable control regulation positive pressurization, and encapsulated nozzle specification 2 regulation or Renewable Food Starch, Sodium and Electrolyte standard nozzle measured in diameter specification of pressurized stream; or 2. Zero system specification air pressurization, control valve variable control regulation positive pressurization, and standard nozzle measured in diameter specification of pressurized stream; or 3. Differential pressurized variable control regulation Surface Treat and Survey Substrate Substances Renewable Food Starch, Sodium and Electrolyte Precision Media System; specification air pressurization, control valve variable control regulation positive pressurization, and encapsulated nozzle specification 2 regulation or Renewable Food Starch, Sodium and Electrolyte standard nozzle measured in diameter specification of pressurized stream; or 4. differential pressurized variable control regulation Surface Treat and Survey Substrate Substances Renewable Food Starch, Sodium and Electrolyte Precision Media System; specification air pressurization, control valve variable control regulation positive pressurization, and encapsulated nozzle specification 2 regulation or Renewable Food Starch, Sodium and Electrolyte standard nozzle measured in diameter specification of pressurized stream; and zero nozzle aqueous slurry system requires no differential pressurization calculation as the exception to the rule.

This system comprises an encapsulated nozzle for advanced efficiency of operation FIG. 9, a standard nozzle FIG. 8, an alternating encapsulated pressurized nozzle for applications requiring two volumes of Renewable Food Starch, Sodium and Electrolyte FIG. 10, in addition to an encapsulated fan nozzle measured in diameter for applications requiring a wide stream of Renewable Food Starch, Sodium and Electrolyte for paint stripping, substrate treatment, parts treatment and cleaning specifications sizes may vary not shown here.

With the addition of a parallel phase regulator switch this system can expand to operate parallel capacities of Renewable Food Starch, Sodium and Electrolyte for applications without interval when necessary FIG. 7. 

1. Description of all parts making and using the same built to specification towards the application specificity requirement sizes may vary Renewable Food Starch, Sodium and Electrolyte aqueous slurry formula zero nozzle aqueous slurry system; 1—Specification aqueous slurry pliable hose line-in measured in diameter from aqueous slurry electronic pump finite or variable control delimited not shown here; with or without specification of pressurized air hose line-in measured in diameter from electronic air compressor pump finite or variable control delimited not shown here; and with or without specification of pressurized air hose line-in measured in diameter to vertical alignment encapsulated nozzle or standard alignment encapsulated nozzle not shown here; 2—with or without bi-interval valve measured in diameter not shown here; and 3—encapsulated nozzle vertical alignment shape nozzle or vertical alignment shape nozzle without encapsulated nozzle aperture measured in diameter, divergence measured in degrees angulation or linear, aperture measured in diameter, or encapsulated nozzle standard alignment shape nozzle or standard alignment shape nozzle without encapsulated nozzle aperture measured in diameter, divergence measured in degrees angulation or linear, aperture measured in diameter, six to ten sides or continuous measured in diameter not shown here.
 2. The specification as set forth comprises electrical component systems rated alternating AC or direct current DC attached to a portable frame with handles and wheels not shown here; electric motor, air compressor, power supply, rated volts alternating current AC; electric motor, vacuum pump, power supply rated volts alternating current AC; electric motor oscillator, power supply rated volts alternating current AC, or pneumatic oscillator, and pressurized variable control air hose line-in measured in diameter; electric motor, vacuum pump wet or dry, power supply rated volts alternating current AC; and an aqueous slurry electronic motor pump finite or variable control delimited, power supply rated volts alternating current AC, or direct current DC battery power; electronic air compressor pump finite or variable control delimited, power supply rated volts alternating current AC, or direct current DC battery power not shown here.
 3. Description of all parts making and using the same built to specification towards the application specificity requirement sizes may vary for Surface Treat and Survey Metallurgy Substrates Renewable Substances Food Starch, Sodium and Electrolyte Precision Media Systems
 1. Renewable Food Starch, Sodium and Electrolyte airtight plastic injection molded preformed gravity feed free flow hopper comprising lid with release valve, air filter, silica gel slots, any combination of cone or parabolic shaped bottom variations for the Renewable Food Starch, Sodium and Electrolyte consistency and size measured in mesh, filtered air gravity feed outlet, or filtered air top feed outlet with or without gravity feed float, or vacuum packed sealed plastic bag;
 2. Control valve or control valve venturi, specification of negative pressurized air, specification of compressed air control, and specification of pneumatic hose line-in and line-out measured in diameter with or without electric blower variable control;
 3. Specification pneumatic hose line-in measured in diameter, and specification of compressed air;
 4. Outer pressurized chamber, specification of compressed air, and variable control regulator compressed air control;
 5. inner pressurized chamber, specification of compressed air, and variable control regulator compressed air control;
 6. Specification pneumatic hose line-out measured in diameter;
 7. Parallel phase regulator switch, specification of compressed air control, specification pneumatic hose line-in left and right measured in diameter, and elbow connectors left and right;
 8. Encapsulated nozzle, specification of pressurized air, encapsulated nozzle O-ring regulator pneumatic connector finite control, encapsulated nozzle regulator 2 specification of compressed air regulated control, nozzle attachments measured in diameter, and aperture measured in diameter; or alternating encapsulated nozzle, alternating encapsulated nozzle two specifications of pressurized air, alternating encapsulated nozzle two O-ring regulators pneumatic connectors finite control, alternating encapsulated nozzle two regulators 2 specification of compressed air regulated control, nozzle attachments measured in diameter, and aperture measured in diameter; or encapsulated fan nozzle for applications requiring a wide stream of Renewable Food Starch, Sodium and Electrolyte for paint stripping, substrate treatment, parts treatment and cleaning specifications of pressurized air, encapsulated nozzle O-ring regulator pneumatic connector finite control, encapsulated nozzle regulator 2 specification of compressed air regulated control, fan nozzle attachments measured in diameter, and aperture measured in diameter; or shop vacuum pump wet and dry plastic injection molded preformed cone shaped and contoured vacuum attachments affixed at the end of the nozzle by way of a shop vacuum pump wet and dry hose line-in measured in diameter;
 9. Wand with nozzle, siphon, or pump, and nozzle attachments measured in diameter;
 10. Water suppressor supply of water hose line-in measured in diameter and fine water suppressor attachments water ring or water ring delimited;
 11. Nozzle measured in diameter specification of pressurized stream;
 12. Plastic injection molded preformed parts cleaning cabinet system; diminishing gravity feed bottom and attachments of the parts cleaning cabinet system not shown here;
 13. Naturally occurring Sodium nitrate NaNO₃ and Sodium Chloride NaCl are derived from natural and renewable resources. All sodium salts are highly soluble renewable source of sodium extracts available in thousands of tons per annum are found in shell fish. Since the only guide to the desirable upper limit of sodium is based upon sodium absorption ratio in common use measure of the proportion of sodium relative to beneficial elements calcium and magnesium the complex ratio can be largely found in shell fish principally clams and oyster shells that are crushed and pulverized to powder and batch processed pasteurization then screened in fine mesh range cloths removing non liquid soluble material while sodium salt is dissolved in water ionizing to sodium ions Na+ and the other part as an anion negative charge so that the sodium then acts independently of the anion, although influenced by salinity and pH. The water is removed by melting and boiling point temperatures, latent evaporation condensing, and fractional distillation to the purity of salt crystalline fine white crystalline powder screened and classified for metallurgy surface treatment, increase yields are also made by the high gelling ability in the presence of calcium citrates chelation of the calcium ions by the citrate ions results in the formation of calcium citrate with sodium ion complexes that are synthesis dilute extraction.
 14. Byproducts of the fruit processing industry are the primary media food ingredient citrus peels, pulps, seeds, and banana peels that are picked-up from large fruit processing plants in carbon dioxide refrigerated trucks. The mass fibrous agricultural waste are specially handled and dumped into vacuum pressurized vats beginning the batch process with dehydration low heating evaporation, and/or supercooled disintegrated to form organogenic crystallographic network and/or crushed, pulverized and classifier screened into grade white crystalline powder base, solution batch classifiers solution batch separate liquid soluble from non liquid soluble material from universal pulp pressing, screening and filtration for clarification non liquid soluble from liquid soluble and/or from dilute extraction soluble. The liquid soluble solutions are suspended in three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch. The three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch solutions may be chemically dehydrated, supercooled disintegrated to form organogenic crystallographic network and classifier screened into grade white crystalline powder base, or low heating evaporated into fine white crystalline powder. The non liquid soluble pulps may be supercooled disintegrated to form organogenic crystallographic network or crushed and classifier screened into three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch and may repeat filtration for clarification non liquid soluble from liquid soluble and/or from dilute extraction soluble. The three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch also may be carbon dioxide super cooled to 0° C. or 32° F. temperatures super cooling refrigeration decelerate temperature to −109° F. degrees Fahrenheit or −78.5° C. degrees Celsius forming organogenic crystallographic network. The three base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate and food starch may be classifier screened into organogenic crystallographic network grade white crystalline powder or supercooled disintegrated to form organogenic crystallographic network or crushed, pulverized and classifier screened into grade white crystalline powder base, and/or from dilute extraction soluble. Base category E Number citric acid E330 and E331 monosodium, disodium and trisodium citrate are initiated by fermentation of peel, pulps and seeds proteins pecin, and pecin citric acid category or sodium citrate category white crystalline powder, cultivated in Vats with the mould Aspergillus niger, incubated with warm heat on ⅛ diurnal cycle incremental mould Aspergillus niger cultivate and lasting for a few days. Step-1 Sodium citrate is formed from reactions of carbonate ions with citric acid and are chelated by the citrate ion of sodium citrate, the process of organic compounds form multiple bonds with a single metal ion, resulting in the formation of complex molecules that are highly soluble, inactive non reacting with other elements or ions to produce precipitates. Step-2 Sodium citrate increase yields are also made by the high gelling ability in the presence of calcium citrates chelation of the calcium ions by the citrate ions results in the formation of calcium citrate with sodium citrate complexes that are dilute extraction soluble. With crystallization techniques and including the sodium citrate chelating technique results in E Number E330 citric acid grade white crystalline powder made in anhydrous form having the property to crystallize from hot water or monohydrate form having the property to crystallize from cold water. Likely the monohydrate form can be converted to the anhydrous form with high heating. The Food Starch, Sodium and Electrolyte base white crystalline powder and liquids comprise a remarkable consecutive incremental yield as many as 8%, 16%, 24% and 48% of the weight of the fruit industry byproduct. 